CN106393479A - Waste paper-aluminum-plastic composite packaging material aluminum-plastic softening agent separation technology - Google Patents
Waste paper-aluminum-plastic composite packaging material aluminum-plastic softening agent separation technology Download PDFInfo
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- CN106393479A CN106393479A CN201610800752.5A CN201610800752A CN106393479A CN 106393479 A CN106393479 A CN 106393479A CN 201610800752 A CN201610800752 A CN 201610800752A CN 106393479 A CN106393479 A CN 106393479A
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- aluminum
- plastic
- tank
- flotation
- plastic film
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- 239000004033 plastic Substances 0.000 title claims abstract description 60
- 229920003023 plastic Polymers 0.000 title claims abstract description 60
- 238000000926 separation method Methods 0.000 title claims abstract description 28
- 239000002699 waste material Substances 0.000 title claims abstract description 17
- 239000011091 composite packaging material Substances 0.000 title claims abstract description 16
- 238000005516 engineering process Methods 0.000 title abstract description 10
- 239000004902 Softening Agent Substances 0.000 title abstract 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 58
- 239000002985 plastic film Substances 0.000 claims abstract description 32
- 229920006255 plastic film Polymers 0.000 claims abstract description 32
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 31
- 238000006243 chemical reaction Methods 0.000 claims abstract description 21
- 238000000034 method Methods 0.000 claims abstract description 21
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000005260 corrosion Methods 0.000 claims abstract description 11
- 230000007797 corrosion Effects 0.000 claims abstract description 11
- 239000003112 inhibitor Substances 0.000 claims abstract description 7
- 239000011888 foil Substances 0.000 claims abstract description 6
- 238000005469 granulation Methods 0.000 claims abstract description 6
- 230000003179 granulation Effects 0.000 claims abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 238000005188 flotation Methods 0.000 claims description 36
- 239000002893 slag Substances 0.000 claims description 36
- 239000000463 material Substances 0.000 claims description 11
- 239000012535 impurity Substances 0.000 claims description 8
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 claims description 8
- 238000000746 purification Methods 0.000 claims description 5
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical group COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 claims description 4
- 239000002131 composite material Substances 0.000 claims description 4
- 235000019253 formic acid Nutrition 0.000 claims description 4
- 244000007853 Sarothamnus scoparius Species 0.000 claims description 3
- 239000000853 adhesive Substances 0.000 claims description 3
- 230000001070 adhesive effect Effects 0.000 claims description 3
- 239000003945 anionic surfactant Substances 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 3
- 238000005202 decontamination Methods 0.000 claims description 3
- 230000003588 decontaminative effect Effects 0.000 claims description 3
- 238000007667 floating Methods 0.000 claims description 3
- 239000013502 plastic waste Substances 0.000 claims description 3
- 239000012141 concentrate Substances 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims description 2
- 239000000284 extract Substances 0.000 claims description 2
- 239000010893 paper waste Substances 0.000 claims description 2
- 238000001291 vacuum drying Methods 0.000 claims 1
- 238000004064 recycling Methods 0.000 abstract description 11
- 230000009286 beneficial effect Effects 0.000 abstract description 4
- 238000004140 cleaning Methods 0.000 abstract description 3
- 238000001035 drying Methods 0.000 abstract description 3
- 230000005764 inhibitory process Effects 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 2
- 230000005484 gravity Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000008267 milk Substances 0.000 description 2
- 210000004080 milk Anatomy 0.000 description 2
- 235000013336 milk Nutrition 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 239000013543 active substance Substances 0.000 description 1
- 239000012790 adhesive layer Substances 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000005453 pelletization Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000009991 scouring Methods 0.000 description 1
- 235000014214 soft drink Nutrition 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/02—Separating plastics from other materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B2017/001—Pretreating the materials before recovery
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- Processing Of Solid Wastes (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种废旧的纸铝塑复合包装中铝塑分离的工艺方法,特别是涉及一种废旧利乐包中铝塑分离的工艺方法。The invention relates to a process method for separating aluminum and plastic in waste paper-aluminum-plastic composite packaging, in particular to a process method for separating aluminum and plastic in waste Tetra Pak.
背景技术Background technique
近年来,随着全球经济的不断发展,各国对果饮品、牛奶等市场需求不断加大,软饮包、奶盒等利乐包废弃物也随之增加,对环境和资源造成了一定的压力。废旧纸铝塑复合包装材料回收利用是资源再生的一条重要途径,对利乐包中的铝、纸、塑等主要成分进行回收再利用,不仅可以缓解环境压力,还能给相关企业带来经济巨大经济效益;由于纸、塑料、铝箔等性质差异较大,为了高效回收利用这类利乐包,首先必须将它们进行有效的分离。当前,对于利乐包类的纸铝塑分离技术主要存在的问题有分离不够彻底导致产品纯度不高、分离工艺系统不够完善,回收产品不够全面以及分离工艺无法进行产业化等主要问题。因此亟需一种新型的、可产业化的废旧铝塑分离工艺方法,从而实现对利乐包的回收循环再利用。In recent years, with the continuous development of the global economy, the market demand for fruit drinks and milk in various countries has continued to increase, and Tetra Pak waste such as soft drink bags and milk boxes has also increased, which has caused certain pressure on the environment and resources. . Recycling waste paper-aluminum-plastic composite packaging materials is an important way to regenerate resources. Recycling and reusing the main components such as aluminum, paper, and plastic in Tetra Pak can not only relieve environmental pressure, but also bring economic benefits to related companies. Huge economic benefits; due to the large differences in the properties of paper, plastic, aluminum foil, etc., in order to efficiently recycle this type of Tetra Pak, they must first be effectively separated. At present, the main problems in the paper-aluminum-plastic separation technology of Tetra Pak are that the separation is not thorough enough to result in low product purity, the separation process system is not perfect, the recovery of products is not comprehensive enough, and the separation process cannot be industrialized. Therefore, there is an urgent need for a novel, industrializable waste aluminum-plastic separation process, so as to realize the recycling of Tetra Pak.
发明内容Contents of the invention
鉴于目前对利乐包等复合包装材料中的铝塑分离技术所面临的上述问题,本发明的目的是设计一种能实现对利乐包等复合包装材料中铝塑膜进行高效的、连续式的、可产业化的分离工艺方法。本发明为同期申请的“一种混杂铝纸塑复合包装材料分质增值工艺系统”子专利,作为纸塑分离工艺中产生的铝塑料膜后续处理工艺。In view of the above-mentioned problems currently faced by the aluminum-plastic separation technology in composite packaging materials such as Tetra Pak, the purpose of the present invention is to design a kind of efficient and continuous separation of aluminum-plastic films in composite packaging materials such as Tetra Pak. A separation process method that can be industrialized. The invention is a sub-patent of "a hybrid aluminum-paper-plastic composite packaging material quality-added value-added process system" applied at the same time, which is used as a subsequent treatment process for the aluminum-plastic film produced in the paper-plastic separation process.
本发明的目的是这样实现的,所述的一种废旧纸铝塑复合包装材料铝塑软化剂分离的工艺,包括如下步骤:1)通过纸塑分离工艺去除纸浆后铝塑复合材料首先进入反应罐,通过反应罐内的双向旋转的内套筒进行进料和出料,反应罐内在进料前预先注入软化剂和缓蚀剂,进料结束后内筒通过不断旋转促进铝塑膜和软化剂接触,同时外套筒表有镂空部分注入热水加速软化剂和铝塑间热粘合剂的反应进程,反应约0.4-1h后,反应罐内容转变旋转方向进行出料;2)反应后相互剥离后的铝塑料膜经过双向绞龙传送至铝塑分选机中,在机械作用下不断将铝箔破碎且大部分附着于塑料膜上,而后铝塑膜通过导料系统进入铝塑分选机,通过高速离心甩脱及水的冲刷作用,附着在塑料膜上的铝屑与水形成铝屑液并汇集到铝粉缓冲池,缓冲池中铝粉液进入铝粉提纯系统;4)经过铝粉提纯系统的旋流分离去除杂质、固液分离器螺旋浓缩提取铝粉及最真空干燥后得到清洁、高纯度的铝粉;5)而去除铝屑后的塑料薄膜经过挤干压包后用于薄膜造粒系统得到再生塑料。The purpose of the present invention is achieved in this way. The process for separating the aluminum-plastic softener of the waste paper-aluminum-plastic composite packaging material includes the following steps: 1) After removing the pulp through the paper-plastic separation process, the aluminum-plastic composite material first enters the reaction The tank is fed and discharged through the two-way rotating inner sleeve in the reaction tank. The softener and corrosion inhibitor are pre-filled in the reaction tank before feeding. At the same time, there is a hollow part on the surface of the outer sleeve to inject hot water to accelerate the reaction process of the softener and the thermal adhesive between aluminum and plastic. After about 0.4-1h of reaction, the content of the reaction tank changes the direction of rotation and discharges; 2) After the reaction, the mutual The peeled aluminum-plastic film is sent to the aluminum-plastic separator through the two-way auger, and the aluminum foil is continuously broken under mechanical action and most of it is attached to the plastic film, and then the aluminum-plastic film enters the aluminum-plastic separator through the material guide system , through high-speed centrifugal separation and water scouring, the aluminum scrap attached to the plastic film and water form an aluminum scrap liquid and collect it into the aluminum powder buffer pool, and the aluminum powder liquid in the buffer pool enters the aluminum powder purification system; 4) after the aluminum The cyclone separation of the powder purification system removes impurities, the solid-liquid separator spirally concentrates and extracts aluminum powder and the most vacuum-dried to obtain clean, high-purity aluminum powder; Recycled plastics are obtained in a film pelletizing system.
所述软化剂的主要成分为甲酸。The main component of the softener is formic acid.
所述缓蚀剂为一种阴离子表面活性剂。The corrosion inhibitor is an anionic surfactant.
本发明所述的一种废旧纸铝塑复合包装材料铝塑分离的设备,包括进料浮选模块、捞料模块及溢流排渣模块;其特征在于:The equipment for separating aluminum and plastic of waste paper, aluminum and plastic composite packaging materials according to the present invention includes a feed flotation module, a material fishing module and an overflow slag discharge module; it is characterized in that:
1)进料浮选模块主要由进水管道、进料口、浮选池和鼓气管组成,所述的进水管道通过蓄水池外的水泵将纸铝塑废渣和水体送入浮选池内,进料口设置在浮选池的入水口的进水管道上方,浮选池的入水口位于池壁中上方处;鼓气管设置在浮选池体梯面的中部,距离集渣槽底部0.4~1米处;1) The feed flotation module is mainly composed of a water inlet pipe, a feed inlet, a flotation tank and an air blast pipe. The water inlet pipe sends paper, aluminum and plastic waste residue and water into the flotation tank through a pump outside the reservoir , the feed inlet is set above the water inlet pipe of the water inlet of the flotation tank, and the water inlet of the flotation tank is located at the upper middle of the pool wall; the gas blowing pipe is set in the middle of the step surface of the flotation tank body, 0.4 from the bottom of the slag collection tank ~1 meter;
2)捞料模块主要由捞渣板和集料槽组成,所述捞渣板由板柄及须状塑料构成,其形状类似于扫帚,须状塑料伸入浮选池液面之下,通过电机传动进行360°旋转;所述集料槽设于高于浮选池中水体液面的2-5cm处,集料槽底部设置为倾斜状,便于碎膜的收集,捞渣板在旋转的过程中可将浮在水面上的塑料碎膜不断推入集料槽;2) The material removal module is mainly composed of a slag removal board and a collection tank. The slag removal board is composed of a plate handle and whisker-shaped plastics. Its shape is similar to a broom. The motor drives to rotate 360°; the collection tank is set at 2-5cm higher than the water level in the flotation tank, and the bottom of the collection tank is set in an inclined shape to facilitate the collection of broken films. During the process, the broken plastic film floating on the water surface can be continuously pushed into the collection tank;
3)溢流排渣模块主要由溢流管、溢流排水口、集渣槽及排渣口组成,所述的溢流管顶端设置有溢流口,浮选水通过溢流管后经溢流排水口排入蓄水池,浮选水经过简易的处理后能不断进行循环利用;所述集渣槽位于浮选池底部,收集的杂质能通过定时打开集渣槽底部设有的排渣口进行排杂。3) The overflow slag discharge module is mainly composed of an overflow pipe, an overflow drain outlet, a slag collection tank and a slag discharge port. The top of the overflow pipe is provided with an overflow port. The flotation water can be continuously recycled after simple treatment; the slag collection tank is located at the bottom of the flotation tank, and the collected impurities can be discharged by regularly opening the slag discharge tank at the bottom of the slag collection tank. Mouth for decontamination.
本发明的有益效果是:本发明主要包括:铝塑分离、再生塑料膜和再生铝粉三个模块,便可实现对利乐包等复合包装材料进行铝塑分离、塑料膜清洗回收、铝粉浓缩干燥回收;通过软化剂(自主研发的试剂,主要成分为甲酸)与复合包装材料中的铝塑料膜之间的热粘合层反应,利于后端工艺中铝塑的分离效率;通过缓蚀剂(一种阴离子表明活性剂)缓解软化剂对铝箔的腐蚀作用,缓蚀效率可达99.7%,利于提高后端回收铝粉的纯度。该工艺产生的软化剂废液可通过补给等简易处理后循环使用;该工艺得到的铝粉纯度可达99.99%,利用价值高;该工艺得到的再生塑料膜直接通过热风风送分质增值造粒系统。通过连续式地重力浮选和“微气泡”浮选共同作用选来实现废旧碎渣的分选,提高塑料碎膜的回收利用率。通过重力浮选和“微气泡”气浮的双重作用不但大大提高了回收碎膜的纯度而且最大程度降低了回收的运行成本,使获得的碎膜更加洁净,节约了碎渣的清洗时间,同时通过连续式的工作方式大大提高了工作效率,此外本发明中设置有溢流口,浮选用水可循环利用率高。同时,该设备结构简单,制造成本低,适合各大相关企业采用。The beneficial effects of the present invention are: the present invention mainly includes three modules: aluminum-plastic separation, recycled plastic film and recycled aluminum powder, which can realize aluminum-plastic separation, plastic film cleaning and recycling, aluminum powder and other composite packaging materials such as Tetra Pak. Concentration, drying and recovery; through the reaction of the thermal adhesive layer between the softener (a self-developed reagent, the main component is formic acid) and the aluminum-plastic film in the composite packaging material, it is beneficial to the separation efficiency of aluminum-plastic in the back-end process; through corrosion inhibition Agent (an anionic active agent) relieves the corrosion effect of softener on aluminum foil, and the corrosion inhibition efficiency can reach 99.7%, which is beneficial to improve the purity of aluminum powder recovered at the back end. The softener waste liquid produced by this process can be recycled after simple treatment such as replenishment; the purity of aluminum powder obtained by this process can reach 99.99%, and has high utilization value; the recycled plastic film obtained by this process is directly sent by hot air to separate quality and increase value. granular system. Through continuous gravity flotation and "micro-bubble" flotation, the separation of waste and debris can be realized, and the recycling rate of plastic film can be improved. The dual effects of gravity flotation and "micro-bubble" air flotation not only greatly improve the purity of the recovered shredded film, but also reduce the operating cost of recycling to the greatest extent, making the obtained shredded film cleaner and saving the cleaning time of the debris. The working efficiency is greatly improved by the continuous working mode. In addition, an overflow port is provided in the present invention, and the flotation water can be recycled with high utilization rate. At the same time, the device has a simple structure and low manufacturing cost, and is suitable for use by major related enterprises.
附图说明Description of drawings
图1是本发明设计的主体工艺流程图。Fig. 1 is the main process flow chart of the present invention's design.
具体实施方式detailed description
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.
图1:铝塑分离工艺方法流程图:通过纸塑分离工艺去除纸浆后铝塑复合材料首先进入反应罐,(该设备为双向滚筒式反应罐,已申请专利,申请号:201220599505.0)通过反应罐内的双向旋转的内套筒进行进料和出料,反应罐内在进料前预先注入软化剂(本发明主要成分为甲酸,软化剂可以采用本领域常规的配方)和缓蚀剂(本发明采用常规的阴离子表面活性剂,缓蚀剂可以采用本领域常规的配方),进料结束后内筒通过不断旋转促进铝塑膜和软化剂接触,同时外套筒表有镂空部分注入热水加速软化剂和铝塑间热粘合剂的反应进程。反应约0.4-1h后,反应罐内容转变旋转方向进行出料,反应后相互剥离后的铝塑料膜经过双向绞龙传送至铝塑分选机中,铝塑分选机与纸塑分选机机理相似,主要是通过高速冲刷淋洗、甩脱的作用,该设备已申请专利(申请号:201220382836.9),在机械作用下不断将铝箔破碎且大部分附着于塑料膜上,而后铝塑膜通过导料系统进入铝塑分选机,通过高速离心甩脱及水的冲刷作用,附着在塑料膜上的铝屑与水形成铝屑液并汇集到铝粉缓冲池,缓冲池中铝粉液进入铝粉提纯系统,该系统包括铝液缓冲池,浓缩池、铝粉干燥器,其中铝粉干燥器为现有技术,经过旋流分离去除杂质、固液分离器螺旋浓缩提取铝粉及最真空干燥后得到清洁、高纯度的铝粉;而去除铝屑后的塑料薄膜经过挤干压包后用于薄膜造粒系统(现有的基础造粒技术,本发明所指是三阶单螺杆造粒系统)得到再生塑料。Figure 1: Flow chart of the aluminum-plastic separation process: After removing the pulp through the paper-plastic separation process, the aluminum-plastic composite material first enters the reaction tank, (this equipment is a two-way drum reaction tank, and has applied for a patent, application number: 201220599505.0) through the reaction tank The two-way rotating inner sleeve in the inner sleeve is used for feeding and discharging, and the softener (the main component of the invention is formic acid, and the softener can adopt the conventional formula in this field) and corrosion inhibitor (the invention uses Conventional anionic surfactants and corrosion inhibitors can use conventional formulations in this field), after the feeding is completed, the inner cylinder is continuously rotated to promote the contact between the aluminum plastic film and the softener, and at the same time, there is a hollow part on the surface of the outer sleeve to inject hot water to accelerate softening The reaction process of the agent and the thermal adhesive between aluminum and plastic. After reacting for about 0.4-1h, the content of the reaction tank changes the direction of rotation to discharge the material. After the reaction, the aluminum-plastic film peeled off from each other is sent to the aluminum-plastic separator through a two-way auger. The aluminum-plastic separator and the paper-plastic separator The mechanism is similar, mainly through high-speed washing, rinsing and throwing off. This equipment has applied for a patent (application number: 201220382836.9). Under mechanical action, the aluminum foil is continuously broken and most of it is attached to the plastic film, and then the aluminum-plastic film passes through The material guide system enters the aluminum-plastic sorting machine. Through high-speed centrifugal separation and water washing, the aluminum scrap attached to the plastic film and water form an aluminum scrap liquid and collect it into the aluminum powder buffer pool. The aluminum powder liquid in the buffer pool enters the Aluminum powder purification system, the system includes aluminum liquid buffer pool, concentration pool, aluminum powder dryer, among which the aluminum powder dryer is the existing technology, through cyclone separation to remove impurities, solid-liquid separator spiral concentration to extract aluminum powder and the most vacuum Clean, high-purity aluminum powder is obtained after drying; and the plastic film after removing the aluminum scrap is squeezed dry and packed and then used in the film granulation system (the existing basic granulation technology, the present invention refers to the three-stage single-screw granulation system) granulation system) to obtain recycled plastics.
实施案例:厦门陆海环保股份有限公司。铝塑分离工艺中铝塑膜日处理量为60t/天(湿重,含水率约为40-50%),塑料膜产品含铝率为1-1.2%、含杂率1.3-2.2%;铝粉产量10t/天,铝粉纯度达99.99%。Implementation case: Xiamen Luhai Environmental Protection Co., Ltd. In the aluminum-plastic separation process, the daily processing capacity of aluminum-plastic film is 60t/day (wet weight, moisture content is about 40-50%), the aluminum content of plastic film products is 1-1.2%, and the impurity content is 1.3-2.2%; The powder output is 10t/day, and the purity of aluminum powder reaches 99.99%.
本发明所述的设备,该装置主要包括了进料浮选模块、捞料模块及溢流排渣模块。According to the equipment of the present invention, the device mainly includes a feed flotation module, a material scooping module and an overflow slag discharge module.
1)进料浮选模块主要由进水管道4、进料口3、浮选池5、鼓气管6等主要部件组成,所述的进水管道4通过蓄水池外的水泵将水体送入浮选池内,进料口3设置在浮选池入水口的进水管道上方,纸铝塑废渣和水体一起进入浮选池5(入水口位于池壁中上方);鼓气管6设置在浮选池体梯面的中部,距离集渣槽9底部约0.4~1米处。1) The feed flotation module is mainly composed of main components such as water inlet pipe 4, feed port 3, flotation tank 5, air blowing pipe 6, etc. The water inlet pipe 4 sends the water body into the In the flotation tank, the feed port 3 is set above the water inlet pipe of the flotation tank water inlet, and the paper, aluminum and plastic waste slag enters the flotation tank 5 together with the water body (the water inlet is located above the middle of the tank wall); The middle part of the pool body terrace is about 0.4 to 1 meter away from the bottom of the slag collecting tank 9.
2)捞料模块主要由捞渣板1、集料槽2等组成,所述捞渣板1由板柄及须状塑料构成(类似于扫帚),须状塑料伸入浮选池液面之下,通过电机传动进行360°旋转;所述集料槽2高于液面2-5cm,料槽底部设置为倾斜状,便于碎膜的收集,捞渣板1在旋转的过程中可将浮在水面上的塑料碎膜不断推入集料槽。2) The material removal module is mainly composed of a slag removal board 1, a collection tank 2, etc. The slag removal board 1 is composed of a plate handle and whisker-shaped plastic (similar to a broom), and the whisker-like plastic extends above the liquid surface of the flotation tank Down, rotate 360° by motor drive; the collection tank 2 is 2-5cm higher than the liquid level, and the bottom of the tank is set in an inclined shape to facilitate the collection of broken films. The slag removal plate 1 can remove the floating Plastic film on the surface of the water is constantly pushed into the sump.
3)溢流排渣模块主要由溢流管10、溢流排水口7、集渣槽9、及排渣口8等组成,所述的溢流管10顶端设置有溢流口,浮选水通过溢流管后经排水口排入蓄水池,浮选水经过简易的处理后可不断进行循环利用;所述集渣槽9位于浮选池2底部,收集的杂质可通过定时打开排渣口进行排杂。3) The overflow slag discharge module is mainly composed of an overflow pipe 10, an overflow outlet 7, a slag collection tank 9, and a slag discharge port 8. After passing through the overflow pipe, it is discharged into the reservoir through the drain outlet, and the flotation water can be continuously recycled after simple treatment; the slag collection tank 9 is located at the bottom of the flotation tank 2, and the collected impurities can be discharged by opening regularly Mouth for decontamination.
具体工作原理为:The specific working principle is:
在本设备中,废渣从进料口3下料后在进水水流的推送下一起进入浮选池5,废渣进入浮选池后受到水体的浮力和“微气泡”的“托举”的双重作用,废渣中的碎塑料膜不断上浮,经过捞渣板1的推送作用,料膜不断被输送至集料槽2收集;废渣中的硬质塑料、泥沙及纸木屑等在重力作用下直接沉入浮选池5底部的集渣槽9,通过排渣口8可定时将杂质去除(去除过程中流失的水通过过滤也可直接回用);溢流排水口7排出的水可回流至蓄水池,经过简易处理后通过泵送直接回用,循环利用率高。In this equipment, the waste slag enters the flotation tank 5 under the push of the water flow after being discharged from the feed port 3. function, the broken plastic film in the waste slag continuously floats up, and through the pushing action of the slag removal board 1, the material film is continuously transported to the collection tank 2 for collection; the hard plastic, silt and paper sawdust in the waste slag are directly discharged under the action of gravity. Sink into the slag collection tank 9 at the bottom of the flotation tank 5, and the impurities can be removed regularly through the slag discharge port 8 (the water lost during the removal process can also be directly reused through filtration); the water discharged from the overflow drain 7 can be returned to The storage tank is directly reused by pumping after simple treatment, and the recycling rate is high.
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